US 5,025,634 A · Heating and cooling apparatus

Abstract

A heating and cooling method and apparatus for a single, closed loop configuration for directly exchanging thermal energy with the earth for both heating and cooling purposes. A refrigerant, which is pumped through the apparatus by a compressor, undergoes two phase transitions during each circuit through the loop. A subterranean heat exchanger has a pair of manifolds in flow communication with a plurality of substantially horizontally oriented tubes. Refrigerant flowing through the tubes has sufficient velocity to sweep lubricant oil, which has escaped from the compressor, along with it for return to the compressor. An expansion valving assembly automatically meters and regulates the flow rate and pressure of the refrigerant during both the heating mode and the cooling mode of the apparatus. A refrigerant storage device automatically supplies or accepts the change in quantity of the refrigerant required when the apparatus changes from either the heating or cooling mode to the reverse mode. A bypass mechanism anticipates the low pressure condition which arises at the compressor input during reversal or startup of the apparatus and provides multiple attempts to overcome inertial resistance corresponding thereto. A modified embodiment of the apparatus provides a non-phase-change heat exchanger flow communicating in tandem to remove a portion of the thermal energy for auxiliary thermodynamic purposes.

Claims22

Dependent claims

In a heating and cooling apparatus having a subterranean heat exchanger in thermal communication with the earth, a dynamic load heat exchanger in thermal communication with a dynamic load, a refrigerant for conveying thermal energy through said apparatus, said refrigerant alternately undergoing gas-to-liquid and liquid-to-gas phase changes while being directed through said apparatus, and a compressor for cycling said refrigerant through said apparatus, said compressor containing a lubricant, the improvement comprising:

(a) said subterranean heat exchanger being oriented substantially horizontally and including a pair of manifolds and a plurality of tubes fluidically interconnecting said manifolds;
(b) reversing valve means for selectively and reversibly interconnecting said compressor with said subterranean heat exchanger and said dynamic load heat exchanger for reversing the direction and sequence of refrigerant flow through said heat exchangers;
and
(c) lubricant recovery means for recovering said lubricant from said subterranean exchanger and for restoring said recovered lubricant to said compressor.

1 more element

(a) said subterranean heat exchanger being oriented substantially horizontally;
(b) reversing valve means for selectively and reversibly interconnecting said compressor with said subterranean heat exchanger and said dynamic load heat exchanger for reversing the direction and sequence of refrigerant flow through said heat exchangers;
(c) lubricant recovery means for recovering said lubricant from said subterranean exchanger and for restoring said recovered lubricant to said compressor;
(d) said subterranean heat exchanger having a pair of manifolds;
(e) a tube fluidically connecting said manifolds;
and
(f) a plurality of tubes having substantially equal lengths and equal diameters wherein a first end of each tube of said plurality of tubes is rigidly secured to and in flow communication with a first manifold of said pair of manifolds and a second end of each tube of said plurality of tubes is rigidly secured to and in flow communication with a second manifold of said pair of manifolds, and wherein said first end of a first tube of said plurality of tubes is spaced nearest to said inlet of said first manifold and said second end of said first tube is spaced farthest from said inlet of said second manifold, said first end of a second tube of said plurality of tubes is spaced next nearest to said inlet of said first manifold and said second end of said second tube is spaced next farthest from said inlet of said second manifold, and each successive tube of said plurality of tubes is similarly spaced relative to said inlets of said pair of said manifolds, including the last tube of said plurality of tubes wherein said first end of said last tube is spaced farthest from said inlet of said first manifold and said second end of said last tube is spaced nearest to said inlet of said second manifold.

4 more elements

A heating and cooling apparatus comprising:

(a) a single closed loop structure which comprises:
a temperature control device and a refrigerant compression device, which is in flow communication with a subterranean heat exchanger, which is in flow communication with a dynamic load heat exchanger, which is in flow communication with a reversing valve assembly, which is in flow communication with an expansion valving mechanism, which is in flow communication with a refrigerant storage device;
(b) said apparatus having a heating mode for heating purposes and a cooling mode for cooling purposes;
(c) said refrigerant compression device adapted to cause a refrigerant to flow through said closed loop;
said refrigerant compression device comprising a mechanism for anticipating and compensating for operable low pressure conditions at an input thereof;
(d) said subterranean heat exchanger being substantially horizontally disposed, embedded, and spaced subterraneanly in the earth at least one foot below a local mean frost-line;
said subterranean heat exchanger comprising a pair of manifolds rigidly secured to an in flow communication with a plurality of substantially parallel tubes spaced at least 6 inches apart from each other;
said tubes having substantially equal lengths and equal diameters;
each of said tubes being rigidly secured to and in flow communication with each of said manifolds such that a first end of a first tube of said plurality of said tubes is spaced nearest to an inlet of a first manifold of said pair of manifolds and a second end of said first tube is spaced farthest from an inlet of a second manifold of said pair of manifolds, and a first end of a second tube of said plurality of said tubes is spaced next nearest to said inlet of said first manifold and a second end of said second tube is spaced next farthest from said inlet of said second manifold, and each successive tube of said plurality of said tubes is similarly spaced relative to said inlets of said first and said second manifolds including a last tube of said plurality of said tubes wherein a first end of said last tube is spaced farthest from said inlet of said first manifold and a second end of said last tube is spaced nearest to said inlet of said second manifold;
said tubes adapted to thermally react with the earth thereabout such that said refrigerant passing therethrough substantially operably undergoes a phase change transition from liquid to gas during a heating mode of said apparatus and undergoes a phase transition from gas to liquid during a cooling mode of said apparatus prior to exiting from said tubes;
said tubes further adapted to cause said refrigerant to pass therethrough with sufficient velocity to prevent accumulation therein of lubricant oil which has escaped from said refrigerant compression device;
said subterranean heat exchanger adapted to extract thermal energy from the earth during a heating mode of said apparatus;
said subterranean heat exchanger adapted to dissipate thermal energy into the earth during a cooling mode of said apparatus;
(e) said dynamic load exchanger adapted to provide thermal energy to a receiving medium for further disposition during a heating mode of said apparatus;
said dynamic load heat exchanger adapted to extract thermal energy from said receiving medium during a cooling mode of said apparatus;
said dynamic load heat exchanger adapted to provide a desired rate and quantity of thermal energy exchange with said receiving medium;
said dynamic load heat exchanger adapted to thermally react with said receiving medium such that the refrigerant passing therethrough substantially undergoes a phase transition from gas to liquid during a heating mode of said apparatus and undergoes a phase transition from liquid to gas during a cooling mode of said apparatus prior to exiting from said dynamic load heat exchanger;
(f) said reversing valve assembly having a first configuration for said heating mode of said apparatus wherein said refrigerant received from said refrigerant compression device is sequentially routed first through said dynamic load heat exchanger then through said subterranean heat exchanger, and a second configuration for said cooling mode of said apparatus wherein said refrigerant received from said refrigerant compression device is sequentially routed first through said subterranean heat exchanger then through said dynamic load heat exchanger;
(g) said temperature control device adapted to activate said apparatus when a demand for energy transfer is sensed and to deactivate said apparatus when said demand is satisfied;
said temperature control device adapted to activate said first configuration of said reversing valve assembly when said apparatus is operating in said heating mode, and to activate said second configuration of said reversing valve assembly when said apparatus is operating in said cooling mode;
(h) said expansion valving assembly spaced between said subterranean heat exchanger and said dynamic load heat exchanger;
said expansion valving assembly comprising a heating mode branch and a cooling mode branch;
said heating mode branch permitting said refrigerant to operably flow therethrough during said heating mode of said apparatus and restricting said refrigerant from operably flowing therethrough during said cooling mode of said apparatus;
said heating mode branch comprising a first metering device for regulating the flow rate and pressure of said refrigerant while flowing from said dynamic load heat exchanger to said subterranean heat exchanger;
said cooling mode branch restricting said refrigerant from operably flowing therethrough during said heating mode of said apparatus and permitting said refrigerant to flow therethrough during said cooling mode of said apparatus;
said cooling mode branch comprising a second metering device for regulating the flow rate and pressure of said refrigerant while flowing from said subterranean heat exchanger to said dynamic load heat exchanger;
said heating mode and said cooling mode branch each adapted to equalize pressure thereacross during each off cycle of said apparatus;
and
(i) said refrigerant storage device spaced between said refrigerant compression device and said reversing valve assembly;
said refrigerant storage device having an inlet and an outlet;
said outlet extending internally within said refrigerant storage device and opening in close proximity to an upper extremity of a cavity contained within said refrigerant storage device;
said outlet having an orifice spaced in close proximity to a lowest extremity of said cavity;
said refrigerant storage device adapted to automatically supply said refrigerant to said apparatus when said apparatus changes to one of said heating and cooling modes which operably requires a greater quantity of said refrigerant and to automatically receive said refrigerant from said apparatus when said apparatus changes to the other of said heating and cooling modes which operably requires a lesser quantity of said refrigerant.

30 more elements

A method for extracting thermal energy from the earth for heating purposes and diverting thermal energy to the earth for cooling purposes, comprising the steps of:

(a) providing a thermostatically controlled, single closed loop system containing a refrigerant, said loop having a gaseous portion whereat said refrigerant is substantially in a gaseous phase, and a liquid portion whereat said refrigerant is substantially in a liquid phase;
a dynamic load heat exchanger disposed in said loop at a first juncture between said gaseous portion and said liquid portion;
a subterranean heat exchanger similarly disposed in said loop at a second juncture between said gaseous portion and said liquid portion;
said subterranean heat exchanger substantially horizontally oriented and disposed below the frost-line of the locality;
a compressor for cycling said refrigerant through said loop and a reversing valve assembly having a heating mode configuration for extracting thermal energy from the earth and a cooling mode configuration for diverting thermal energy to the earth;
(b) placing said reversing valve assembly in said heating mode configuration;
followed by
(1) compressing said refrigerant in said gaseous portion with said compressor such that said refrigerant acquires a temperature which is substantially warmer than a receiving medium which is in thermal communication with said dynamic load heat exchanger;
(2) removing thermal energy from said refrigerant by conveying said refrigerant through said dynamic load heat exchanger wherein said refrigerant substantially undergoes a gas-to-liquid phase transition while simultaneously transferring said thermal energy to said receiving medium for distribution elsewhere for heating purposes;
(3) simultaneously controllably regulating the flow rate and reducing the pressure of said liquid refrigerant such that the effective temperature of said refrigerant is substantially less than the temperature of the earth below the frost-line of the locality;
(4) extracting thermal energy from the earth with said refrigerant by passing said refrigerant at a relatively high velocity through said subterranean heat exchanger;
said velocity of said refrigerant sufficient to sweep any lubricant oil, which may have escaped from said compressor along with said lubricant;
said refrigerant substantially undergoing a liquid-to-gas phase transition by absorbing thermal energy from the earth while passing through said subterranean heat exchanger;
(5) returning said refrigerant with said escaped lubricant oil to said compressor completing the cycle of said refrigerant through said single closed loop system and restoring said escaped lubricant oil to said compressor;
(c) placing said reversing valve assembly in said cooling mode configuration;
followed by:
(1) compressing said refrigerant in said gaseous portion with said compressor such that said refrigerant acquires a temperature which is substantially warmer than the earth which is in thermal communication with said subterranean heat exchanger;
(2) diverting thermal energy to the earth from said refrigerant by conveying said refrigerant through said subterranean heat exchanger wherein said refrigerant is conveyed therethrough with sufficient velocity to sweep any said escaped lubricant oil along with said refrigerant;
said refrigerant substantially undergoing a gas-to-liquid phase transition while passing through said subterranean heat exchanger;
(3) simultaneously controllably regulating the flow rate and reducing the pressure of said liquid refrigerant such that the effective temperature of said refrigerant is substantially less than the temperature of said receiving medium in thermal communication with said dynamic load heat exchanger;
(4) absorbing thermal energy from and cooling said receiving medium by conveying said refrigerant through said dynamic load heat exchanger;
said refrigerant substantially undergoing a liquid-to-gas phase transition while passing through said dynamic load heat exchanger;
(5) returning said refrigerant with said extracted lubricant oil to said compressor completing the cycle of said refrigerant through said single closed loop system and restoring said escaped lubricant oil to said compressor.

20 more elements

Dependencies are inferred from the claim text.

Heating and cooling apparatus

Life of this patent

Heating and cooling apparatus

Life of this patent

Abstract

Claims22